The object of the invention is a "process and devices for the constant emission of volatile liquids".
The process proposed by the invention is based on the absorption of volatile liquids through solid absorbents made of diverse materials of a different nature and composition.
At present, volatile liquid products such as insecticides, aromatic substances, disinfectants, phytosanitary products, semochemicals, etc., are dispersed with the use of dispersing products or generally manually, mechanically, thermoelectrically or otherwise activated devices requiring permanent attention which in many case renders their use impracticable. On the other hand, these dispersing devices fail to provide a constant emission of the volatile product in question.
In specific cases where the product must be dispersed over extended areas of farm or woodland, applying these products requires a large number of special machines and propellents almost impossible to install, particularly in places that are not readily accessible.
Known dispersers of a scientific nature based on fluid mechanics or physics fail to provide satisfactory results in equatorial or tropical environments with extremely high diurnal temperatures, high levels of relative humidity, abrupt temperature falls during the dusk and night hours and ambient humidities in the order of 100%.
On the other hand, the use of additional driving elements of a mechanical or thermoelectrical nature which could (and in cases do) solve this problem entails high operating costs and the difficulty of reaching almost inaccessible locations lacking electricity or fuel for driving the system.
The invention presents a simple and efficient solution to these problems and proposes the process and special devices described hereunder.
The use of dispersers heretofore available in the market and applied to agricultural and forestry research purposes in moderate continental climates presents several practical inconveniences which may be overcome by manual modifications varying from one case to the other. However, the use of known dispersers in wet equatorial forest environments fails to respond to the minimum expected operational requirements.
Bearing in mind that the research undertaken employed dispersers that were calibrated to some extent, solving the problems encountered in the putting into operation as a result of basic instrument failures was the first step toward executing the work.
As a first step, a thorough examination was carried out to establish the causes that led to known disperser failures essentially deriving from the critical ambient temperature and humidity conditions that prevailed, particularly in the Amazon forest. During diurnal hours, with a constant temperature of 30°C and a relative humidity never under 85%, dispersion of the volatile liquids took place at an extremely high (evaporated volume/time unit) rate. On the contrary, as from dusk, when the relative humidity reached 100% (condensation), the temperature dropped to under 18°C and the condensation water created a tight chamber around the disperser which fully inhibited the evaporation of the volatile liquid to be dispersed.
Since the causes of known disperser failures could not be solved by modifying the dispersers, other devices had to be created.
A disperser was thus created capable of efficiently responding to the required demands.
The results obtained, which solve the problem involving a break in the dispersion caused by a relative humidity of almost 100%, in addition to continuous and regular daily dispersion rates which varied from 0.5 to more than 2 cc, led to the creation of the system proposed in this document.
It should be understood that the invention has multiple sanitary, cosmetic, agricultural, forestry, etc., applications.
The device and method of the present invention are defined in appended claims 1 and 5, respectively.
In the process described, absorption of the volatile liquids, in particular volatile solvents (with or without accompanying solutes), is conducted through solid absorbents from which they emanate in the form of gas by a physical principle involving vapor pressures differences and air drawing, without the weight of the liquid or solvent intervening and resorting neither to motor and thermoelectrical means nor to compressed fluid dispersers.
Through the process of the present invention, constant dispersion of the substances is achieved in a free or controlled manner, depending on the selected option.
The following elements are foreseen for putting the described process to practical use:
The following description provides a better understanding of the object of the invention if contemplated jointly with the attached drawings that show, somewhat schematically and purely in the form of a non-limiting example, the preferred assemblies and details of the devices for a practical embodiment of said object of the invention.
In the drawings:
Figure 1 shows a half-section elevation view along a vertical plane of the perforated tubular element lodging the absorbent mass.
Figure 2 shows an exploded view of the set of elements comprising the overall liquid product emission device.
Figure 3 shows a half-section elevation view along a vertical plane of the grouped set of elements forming the disperser, depicted in a fully assembled manner, its tank containing the liquid product to be dispersed.
Commenting on the drawings, number 1 identifies the tank containing the liquid product, the level of which is identified by 2. In the practical embodiment of the invention, this tank forms a vessel fitted with means 3 for receiving and securely retaining a disk-shaped lid 4 providing a virtually impervious closure; said lid 4 is fitted with a large central hole 5 surrounded by a neck 6 extending along both sides and forming a tubular housing for tightly lodging a tubular cylindrical element 7 endowed with strategically distributed holes 8 throughout its surface. The tubular element 7 contains an absorbent mass 9; said tubular element 7 penetrates perpendicularly in the tank 1, rests on the bottom thereof in a securely upright position and protrudes above the lid 4 along a portion devoid of absorbent mass 9; this free portion forms a chamber 10 into which ambient air penetrates through the holes 8 to displace the gases emitted from the absorbent mass, causing them to flow through the passage located on the center of a closing part 11 tightly adapted onto the upper end of tubular element 7; lastly, said closure part is covered by a bonnet supported by nerves 14 which emerge from an annular sector of base 15 fitted over the lid 11 providing the upper closure of perforated tube 7.
The tank 1 holds the liquid product or composition 2, which may additionally contain other finely divided or solid components, as indicated by number 16.
Following its preparation, the liquid product or composition to be dispersed is fed into the tank 1 up to a specified level 2, optionally incorporating solid or powdered components 16. The tubular body 7 fitted with holes 8 and containing the absorbent mass 9 is inserted perpendicularly in an upright position and is immersed in the liquid which, through the holes 8, impregnates the overall absorbent mass 9, from which it flows in its gaseous state and penetrates the upper chamber 10, from where it is conveyed to passage 12 by the air entering the chamber 10 formed in the upper end of the perforated tubular body 7, to be finally dispersed in the external environment. Over the upper end of tubular body 7 and lid 11 is installed a covering element formed by a substantially conical bonnet 13 supported by vertical nerves 14 which extend from an annular base 15 securely adapted over the lid 11 which closes the upper end of central body 7.